• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The process for extracting rare earths contained in permanent magnets comprises the steps of heat treatment of the permanent magnet, grinding at the end of the heat treatment to obtain particles having a size of less than 2 mm, treatment with stirring of the particles by a solution containing an organic acid, and separation of the liquid phase from the solid phase.
    公开号:FR3052171A1
    申请号:FR1655059
    申请日:2016-06-03
    公开日:2017-12-08
    发明作者:Alain Seron；Nour-Eddine Menad；Dominique Breeze；Marc Gamet
    申请人:BRGM SA；
    IPC主号:
    专利说明:

    1 - Technical field of the invention
    The present invention relates to a process for extracting rare earths contained in permanent magnets, in particular waste electrical and electronic equipment (D3E or WEEE). 2 - State of the art
    WEEE is the fastest growing waste stream, at 2-3% each year. They have a high recycling potential of the materials that compose them (ferrous and non-ferrous metals, rare metals, glasses, plastics ...). These economic and environmental issues justified the establishment of a specific waste management system, based on the principle of extended producer responsibility (REP) for this equipment. Thus the collection and recycling of WEEE is operational in France since July 22, 2005 for professional WEEE, and since November 15, 2006 for household WEEE.
    However some components are poorly or not recycled. This is the case of rare earth permanent magnets found in many everyday objects, such as computers, televisions or mobile phones. These permanent magnets mainly contain neodymium (Nd) alloyed with iron and boron. They may also include dysprosium (Dy) and praseodymium (Pr).
    Many methods have already been proposed for the recycling of rare earths present in used products, whether magnetized or not. However, these modes of recycling do not give complete satisfaction.
    The following documents describe the recovery of rare earths contained in permanent magnets by chlorination or direct fluorination.
    Document CN101817547 proposes to recover the rare earths of a magnet by a process consisting of crushing the magnet, adding to the powder obtained carbon and then putting this mixture in contact with a flow of chlorine gas to produce chlorides of rare earths and a volatile iron chloride. The rare earths are then purified by oxalic precipitation.
    WO 2009/119720 uses a process for immersing the rare earth alloy in a high temperature halogenated molten salt which makes it possible to extract the rare earths in the form of gaseous rare earth halides.
    These two techniques are unattractive given the dangerous nature of the flow of chlorinated or fluorinated gas.
    A second mode of recycling implements a method of fusion.
    JP 2001-335852 is based on the mixture of magnes powder and a fluorinated agent such as NH4F. The whole is heated until it melts. The rare earths are found after cooling in mixture with a slag and can be separated by difference of density.
    JP 2010-199110 uses the same method of recycling by heating until melting and separation of the melted and unmelted fractions. This last fraction is rich in Nd alloy. The major disadvantage of this type of fusion process is related to energy expenditure which induces a high cost.
    The third mode of recycling is based on rare earth extraction by a molten metal. By way of example, the method of document WO 2007/119846 uses the oxidation of magnets then the contact with molten aluminum leading to the formation of a rare earth oxide mixed with a slag and an alloy Fe-B that must be separated later. In this case, the difficulty lies in the delicate management of the aluminothermie reaction.
    Another process uses the strong affinity of magnesium fused with neodymium, unlike iron. The limits here are related to the management of a metal in the gaseous state, and to the energy expenditure that is associated with the process.
    In the context of hydrometallurgical recycling, the process developed in US5362459 consists of dissolving a slag from the NdFeB alloy preparation by electrolysis in a sulphamic acid bath, the bath then being mixed with hydrofluoric acid to precipitate neodymium fluoride.
    This mode of treatment is not suitable for massive forms of magnets and is very expensive from an energy point of view.
    Description of the invention The object of the invention is to propose an alternative method that does not have all or some of these disadvantages and that makes it possible to extract rare earths contained in permanent rare earth magnets, more particularly of the NdFeB type, doped or not, that is to say added, or not, with other rare earths such as Dy and / or Pr.
    Magnets are characterized by the fact that they have magnetic moments. Permanent magnets are magnets that exhibit remanence or persistence of their magnetic moments, that is, they retain their magnetic properties after the removal of a magnetizing field. A permanent magnet is generally made of a hard magnetic material, manufactured, the remanent field and the coercive excitation are large. Permanent magnets almost always contain atoms of at least one of the following chemical elements: iron, cobalt or nickel, or the family of lanthanides (rare earths). The synthetic magnets used in the present invention are produced by sintering an alloy containing rare earth powders which then forms a polarized alloy under an intense field of an electromagnet. Such materials are particularly used in the process according to the invention.
    NdFeB magnets are also known as neodymium magnets. They are mainly composed of an alloy of neodymium, iron and boron (Nd2Fe14B) to form a tetragonal crystalline system.
    Permanent magnets of NdFeB type, when used in the process according to the invention can be contained in industrial waste originating, for example, from the recycling of hard disk drives of PC type central units or of portable computers, loudspeakers, for example mobile phones or computers, small electric motors or be composed of waste permanent magnet production. Such magnets are often surrounded by a layer of nickel. Nevertheless, their coating may be based on other metals such as cobalt, a copper-cobalt alloy, zinc, etc. The same process is applicable to magnets coated with epoxy. For this purpose, the subject of the invention is a process for extracting rare earths contained in a permanent magnet, more particularly of the NdFeB type, with or without rare earths, comprising the steps of: a) heat treatment of the permanent magnet at a temperature greater than or equal to its Curie temperature, b) grinding of the magnet resulting from the heat treatment step, the particles from the grinding being classified to select the particles having 80 to 90% of them size less than 2 mm, c) stirring treatment of the particles selected at the end of the grinding step with a solution containing an organic acid, d) separation of the liquid phase from a possible solid phase at the end of the treatment with the solution containing the acid.
    Advantageously, the liquid phase contains more than 70% by mass of the rare earths of the permanent magnet having undergone the preceding steps of the process.
    Treatment beyond the Curie temperature, that is to say at a temperature generally greater than 300 ° C., preferably between 300 and 400 ° C., and preferably around 350 ° C., makes it possible to demagnetize final magnet, which is advantageous for the rest of the process which is not disturbed by the magnetic properties of the magnets. This treatment is preferably carried out for a period of at least 10 minutes, and preferably between 10 and 40 minutes.
    By grinding is meant fragmentation of the magnet by subjecting it to shock or pressure. The grinding stage makes it possible to obtain magnet powder, the particle size of which is selected so as to promote acid attack and dissolution of the rare earths. Indeed, the size of the particles influences the physicochemical properties of the substrate. The thinner the product, the faster the dissolution, but the manipulation of too fine powders can in some cases present disadvantages at various stages of the process.
    Preferably, the grinding is a gentle grinding, for example decomposed into at least two grinding stages where the first grinding rejects are subjected to a second grinding as described in FIG. 1: a first step to the grinding after which grinding magnet particles are classified in order to select particles whose size is less than 4 or 2 mm, a second step of grinding unselected particles at the end of the first grinding stage, the particles from the second grinding being classified to select the particles having 80 to 90% of them a size less than 2 mm.
    Unlike deep grinding, which is excessive because it produces more ultrafine particles than it should or because it gives a product generally finer than the desired product, the sparing is practiced in order to obtain precisely the granulometry sought.
    The multi-stage grinding avoids the production of fine particles that volatilize, resulting in loss of material. In addition, it implies a lower energy expenditure than the grinding pushed.
    The sparing can be done in one step.
    Preferably, the selection of the particles is carried out by sieving.
    Additional sieving steps can be added to the process, the sieving refusal (unselected particles after milling) being ground again until all of the magnet has reached the required particle size for the step following process.
    Preferably, the particles on which the acid attack is practiced have a size of less than 2 mm for 80% of them, and preferably for 90% of them.
    Preferably, the particles on which the acid attack is performed have a size greater than 0.2 mm for 80% of them, and preferably for 90% of them.
    Advantageously, the grinding is carried out using a shredder, for example a knife mill. The classification is carried out using sieves according to the standard methods.
    According to an alternative embodiment of the invention, the heat treatment steps a) and b) grinding can be substituted by the supply of demagnetized particles having 80 to 90% of them less than 2 mm in size. Such particles may be from ground demagnetized magnets.
    The treatment of the particles with the solution containing an organic acid, or acid attack, dissolves the constituents of the magnet and in particular the rare earths in the solution. It can also lead to a more or less partial dissolution of a coating present on the surface of the magnet. In the case of nickel-based coatings, the dissolution is very limited which makes it possible to separate it, in the form of a solid residue of nickel, at the end of the process.
    This attack is carried out with a solution of organic acid, in particular C1-C10, preferably C1-C5, carboxylic acids having at least one or two carboxyl functions (or radicals). For example, acetic acid, oxalic acid or citric acid, or a mixture thereof are acids which are particularly advantageous for use in the process according to the invention.
    The solvent of the acid is usually water.
    Preferably the acidic solution has a concentration ranging from 5 to 30% by volume, and for example a concentration of about 10%.
    This can lead to total or partial dissolution of the magnet powders and an interesting partition between residual solid and solution of the different constituent elements of the permanent magnets.
    Preferably, during the acid etching, the magnet powder corresponding to particles selected at the end of the heat treatment and grinding steps is added to the acid solution at the rate of 150 g of powder per liter of d solution. 'acid. The acid attack is preferably carried out for a minimum of 1 hour, preferably less than 24 hours, more preferably ranging from 100 to 550 minutes, for example about 420 minutes.
    Preferably, the acid attack (or leaching) is carried out at a temperature ranging from 10 to 50.degree. C., more preferably from 10 to 30.degree. C., and even more preferably at room temperature, that is to say 20.degree. vs. It can be performed under a static atmosphere of air or nitrogen, under air flow or under nitrogen flow. Preferably, the acid attack brings the pH of the solution to a pH of less than 2. The amount of acid to be added is therefore advantageously an amount of acid to achieve such a pH.
    A low pH value increases the kinetics of the dissolution.
    The liquid phase containing the rare earths is then separated from the solid phase if not all the compounds of the powder have dissolved. This is for example the case for magnets surrounded by a layer of nickel, particularly in the presence of a solution of acetic acid. In this case the nickel, associated or not with iron, remains in solid form and can be recovered by simple solid / liquid separation.
    This solid / liquid separation can be carried out by any known method such as centrifugation, (for example at 3500 rpm for 10 minutes), filtration or decantation. At the end of the acid attack, at least a portion of the ferrous fraction of the magnets is passed into solution.
    Preferably, the iron is separated from the rare earths, optionally during an additional step. In this step, the iron can be precipitated while the rare earths remain, at least in part, in the liquid phase.
    To do this, oxygen can be introduced into the solution, for example by bubbling or stirring with an oxygen-containing gas, such as air, or pure oxygen. This mixture promotes the oxidation of iron from oxidation state 2 to degree 3 and thus the precipitation of iron III oxy-hydroxide compounds or oxy-hydroxides at low pH (ie at a pH generally below 4 ). The pH is preferably measured using a pH measurement resolution pH meter of 0.01 units, a resolution of the potential of 1 mV and a measurement resolution of 0.1 ° C, such as Heitolab P310 pH meter from Heito. Preferably for pH measurement, the electrode is Heito brand. The iron is thus precipitated and can be separated from the rare earths by a phase separation step such as filtration, centrifugation or decantation. Advantageously, the pH is kept below 4 by the addition of acid. Preferably, the solution is maintained at a pH allowing the selective precipitation of iron. For example, the pH is chosen between 3 and 4.
    Alternatively or additionally the separation of the iron is obtained by contacting the solution rich in rare earths and iron with materials of biological origin such as oyster shell powder or powder of pine bark. These materials are advantageously used in the form of a fine powder. Such a powder may comprise essentially particles having a size of 0.5 to 5 mm, preferably 0.6 to 2 mm, for example 1.25 mm. The iron separation step may be carried out prior to the liquid / solid separation described in step d) of the process, or following the liquid / solid separation and be followed by a second liquid / solid separation step .
    Preferably, the rare earths extracted by this process are chosen from Nd, Dy and Pr, and a mixture thereof. The subject of the invention is also a method for extracting rare earths contained in demagnetized particles originating from a permanent magnet, more particularly of the NdFeB type, with or without addition of other rare earths, the process comprising the steps of: agitated treatment of the particles with a solution containing an organic acid, separation of the liquid phase from a possible solid phase at the end of the treatment with the solution containing the acid, the liquid phase advantageously containing more than 70% of the rare earths of the permanent magnet having undergone the preceding steps of the method.
    The conditions and steps of demagnetization, obtaining the particles, for example by grinding, the particle size, the treatment with an acid solution and the separation steps leading to the extraction of the rare earths may advantageously be such as those described herein. -before. Similarly, the iron extraction steps can also be applied to this process. The invention also relates to a recycling process incorporating an extraction process according to the invention wherein the permanent magnet comes from industrial waste. The invention also relates to the products obtained directly from the process according to the invention and their subsequent use, in particular in the field of electronics.
    Another object of the invention is a method as described above comprising no chemical reaction steps between the steps of supplying demagnetized and ground magnet particles and the acid etching step.
    Another object of the invention is a process as described above not comprising chemical reaction steps between acid etching and solid / liquid separation and / or precipitation and / or iron fixation steps.
    Another object of the invention is a method as described in Figure 1. This method may incorporate one or more of the features described above. The invention will be better understood on reading the examples, comprising figures, which will follow, which are given solely by way of example.
    Description of the figures:
    FIG. 1 schematizes the extraction method according to one embodiment of the invention of the rare earths present in permanent magnets, similar to the embodiments exemplified in Examples 2 to 4.
    FIG. 2a is a photograph taken under a scanning electron microscope (SEM) of a permanent magnet according to the control example 1.
    FIGS. 2b and 2c are the results of qualitative chemical analysis by scanning electron microscopy - energy dispersive spectroscopy (EDS SEM) carried out on the magnet of example 1, when it is displayed at the SEM.
    FIG. 3 shows the dissolution rates over time of Fe, Nd, Dy and Ni during the acid attack dissolution stage of a process according to the invention which is the subject of Example 2.
    FIG. 4 shows the dissolution rates according to the Fe, Nd and Dy time during the iron precipitation step of a process according to the invention which is the subject of Example 3.
    FIG. 5 shows the dissolution rates according to the Fe, Nd and Dy time during the iron precipitation step of a process according to the invention which is the subject of Example 4.
    Example 1 (Control): Analysis of a permanent magnet without coating
    FIGS. 2a to 2c show the SEM characterization results of a permanent magnet of the NdFeB type, without coating, which has not been subjected to the process according to the invention. The analysis makes it possible to highlight the granular structure of these magnets consisting of sintered Nd2Fe14B phase crystals (low arrow towards FIG. 2c) in the presence of an intergranular phase rich in rare earths (high arrow towards FIG. 2b). In the MEB EDS analysis of a sintered Nd2Fei4B phase crystal (FIG. 2c), the characteristic line of Fe, which is a majority, and Nd, which is well represented, are identified. In the intergranular phase rich in rare earths (FIG. 2b), the emission lines of Nd, Pr and Dy are particularly identified.
    Example 2 Extraction of Rare Earths from Permanent Nickel-Coated Magnets
    Samples of permanent magnets from laptops or fixed (step 1 of the method shown schematically in Figure 1) type Nickel-Iron-Bore magnets (NdFeB) nickel-coated were used. The chemical composition of the NdFeB alloy composing the core of the magnets is as follows: Iron 61.3%, Neodymium 35%, Dysprosium 1.8% and Boron 1.4%.
    These magnets were heat-treated for 20 minutes at a temperature of 350 ° C. in a muffle furnace, that is to say beyond their Curie temperature, with a view to definitively demagnetizing them (step 2 of FIG. process described in Figure 1), so as not to be disturbed in the following process by their magnetic properties. At the end of this heat treatment, the samples were ground so as to obtain a particle size of less than 2 mm.
    The refusal to sieve, that is to say the particles whose particle size was greater than the desired particle size were subjected to a second grinding step (step 4). This grinding in two stages is a gentle grinding.
    Steps 3 and 4 of Figure 1 were carried out using a shredder type mill (RETSCH SM100 type knife mill - from Retsch GmbH, Retsch-Allee 1-5, 42781 Haan, Germany) with a 2 mm sieve. . Particles larger than or equal to 2 mm then underwent a second milling step using the same mill with a 2 mm sieve. At each of steps 3 and 4, the powder was automatically classified on the 2 mm sieve, resulting in a powder such that 100% of the particles were smaller than 2 mm (quartile 10 or d100).
    Subsequently, a sample of 15 g of magnesium powder resulting from this treatment was dispersed in 100 ml of a 10% dilute acetic acid solution to be subjected to an acid attack step, or leaching (step 5). The mixture was stirred for a period of 24 hours, at a temperature of 30 ° C., under a static (ambient) air atmosphere. A kinetic study of the dissolution of rare earths, iron and nickel was conducted. Samples of the acid etching solution were taken during the reaction at the following times: 5min, 15min, 30min, 1h, 3h, 4h, 5h, 6h and 7h. These samples were centrifuged at 3500 rpm for 10 minutes. The supernatant was then filtered through a 0.22 μm syringe filter (step 6) to separate the solid phase from the liquid phase. The resulting metal solutions were then subjected to atomic absorption analysis to determine the concentration of the different dissolved metals.
    The results of the atomic absorption analyzes of the Fe, Ni, Nd and Dy concentration of the solutions resulting from the acid attacks of the various samples taken are illustrated in FIG.
    This kinetic study shows that the dissolution of the rare earths in a weak dilute acid of acetic acid type is almost complete after 420 minutes of treatment. In the case of the nickel which constitutes the coating of the magnet, the dissolution remains very limited. At the end of the step of acid solubilization with acetic acid, the iron was precipitated. This precipitation was carried out by placing the solution in the presence of oxygen which is introduced into the solution by bubbling air. In order to promote the oxidation of iron from oxidation state 2 to degree 3 and thus to precipitate oxide compounds or oxyhydroxide of iron, the pH was adjusted to a pH ranging from 3 to 4 by adding a additional amount of acetic acid to selectively precipitate iron III without precipitating the rare earths. The pH measurement was carried out using a Heito brand pH meter and model P 310, associated with a Heito electrode.
    Examples 3 and 4
    A magnet powder identical to that used in Example 2 was treated in the same manner as in Example 2, except that the acid treatment step was carried out under nitrogen and the separation of iron from the soil. rare has not been done by the presence of oxygen. The rare earth metal solutions obtained after dissolution by acid attack were treated with materials of biological origin which make it possible to optimize the separation of rare earths and iron.
    Example 3 2.5 g of powder obtained by grinding with the aid of a jaw crusher of fragments of maritime pine bark of 20 to 40 mm in length marketed by Castorama and brand Verve (Kingfisher company, 3 Sheldon Square Paddington London W2 6PX), which has been screened at 1.25 mm, were mixed with 50 ml of iron-containing solution and the rare earths obtained after 420 minutes of reaction. The powder suspension in the acid solution of rare earths thus obtained was kept in constant stirring with the aid of a shaker, at 30 ° C. for 24 hours.
    The results of the atomic absorption analysis of Fe, Nd and Dy concentrations present in the successive samples taken over time during this precipitation step are presented in FIG. 4. This figure shows that iron (low curve), the Nd (upper curve) and the Dy (intermediate curve) are fixed by the bark powder in different proportions from each other. Iron is removed from the solution in its entirety, while less than 50% of the rare earths are. This process makes it possible to extract the iron from the solution and to keep a large part of the rare earths in solution.
    EXAMPLE 4 2.5 g Marenne Oléron oyster shells (Protected Geographical Indication - PGI) derived from food consumption and obtained by milling using a jaw crusher, which has been sieved to 1.25 mm , were mixed with 50 ml of solution containing the iron and rare earths obtained. The powder suspension in the acid solution of rare earths thus obtained is kept in constant agitation with the aid of a shaker, at 30 ° C. for 24 hours.
    The results of the atomic absorption analysis of Fe, Nd and Dy concentrations present in the successive samples taken during the time during this precipitation step are presented in FIG. 5. This figure shows that the iron (low curve), the Nd (upper curve) and the Dy (intermediate curve) are fixed by the oyster shell powder in different proportions from each other. Iron is removed from the solution (precipitate) in its entirety, while less than 35% of the rare earths are. This process makes it possible to extract the iron from the solution and to keep a large part of the rare earths in solution. The invention is not limited to the embodiments presented and other embodiments will become apparent to those skilled in the art.
    权利要求:
    Claims (9)
    [1" id="c-fr-0001]
    1. A process for extracting rare earths contained in a permanent magnet, more particularly of NdFeB type, with or without added rare earths, comprising the steps of: a) heat treatment of the permanent magnet at a temperature greater than or equal to its Curie temperature, b) grinding of the magnet resulting from the heat treatment step, the particles originating from grinding being classified to select particles having 80 to 90% of them less than 2 mm in size, c) stirred treatment of the particles selected at the end of the grinding step with a solution containing an organic acid, d) separation of a liquid phase from a solid phase after treatment with the solution containing the acid.
    [2" id="c-fr-0002]
    2. Method according to the preceding claim, the magnet particles resulting from grinding having a size less than 2 mm for 80% of them, and preferably for 90% of them.
    [3" id="c-fr-0003]
    3. A process according to any one of the preceding claims, the organic acid being acetic acid, oxalic acid or citric acid, or a mixture thereof.
    [4" id="c-fr-0004]
    4. Process according to any one of the preceding claims, the acid solution being at a concentration ranging from 5 to 30% by volume, and for example at a concentration of 10%.
    [5" id="c-fr-0005]
    5. Method according to any one of the preceding claims, the treatment with a solution containing the acid being carried out for a minimum duration of 1 hour, preferably less than 24 hours, more preferably ranging from 100 to 420 minutes, for example of about 420 minutes.
    [6" id="c-fr-0006]
    The method of any of the preceding claims, further comprising a step of separating the iron.
    [7" id="c-fr-0007]
    7. Method according to the preceding claim, the iron being separated by precipitation, for example due to the introduction of oxygen, for example by bubbling or stirring an oxygen-containing gas, such as air, or pure oxygen.
    [8" id="c-fr-0008]
    8. The method of claim 6, wherein the iron is separated by contact with materials of biological origin such as oyster shell powder or pine bark powder.
    [9" id="c-fr-0009]
    9. Recycling process incorporating an extraction process according to any one of the preceding claims, wherein the permanent magnet is from industrial waste.
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    同族专利:
    公开号 | 公开日
    US11155898B2|2021-10-26|
    CA3022190A1|2017-12-07|
    EP3464655A1|2019-04-10|
    FR3052171B1|2021-01-01|
    US20210363608A1|2021-11-25|
    US20190169710A1|2019-06-06|
    WO2017207947A1|2017-12-07|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
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    US8323592B2|2008-03-26|2012-12-04|The Foundation For The Promotion Of Industrial Science|Method and apparatus for recovery of rare earth element|
    JP4820423B2|2009-02-23|2011-11-24|有限会社レアメタルズ２１|Method of recovering neodymium magnet from used equipment and neodymium magnet recovered or recycled by the method|
    CN101817547B|2010-05-07|2011-10-05|沈阳工业大学|Method for recovering mixed rare earth chlorides from neodymium iron boron permanent magnet material scraps|
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    WO2017011368A1|2015-07-10|2017-01-19|University Of Houston System|An improved process for the recovery of rare earth metals from permanent magnets|FR3064496A1|2017-03-31|2018-10-05|Centre National De La Recherche Scientifique|USE OF NATURAL MATERIALS OF VEGETABLE ORIGIN RICH IN PHENOLIC ACIDS FOR THE IMPLEMENTATION OF ORGANIC CHEMICAL REACTION AND RECYCLING OF CATALYSTS|
    IT201800005178A1|2018-05-08|2019-11-08|Hydrometallurgical process for the treatment of permanent magnets|
    CN108823436A|2018-07-05|2018-11-16|武汉工程大学|A kind of compound leaching agent of the formates of weathered superficial leaching rare-earth ore|
    法律状态:
    2017-06-26| PLFP| Fee payment|Year of fee payment: 2 |
    2017-12-08| PLSC| Publication of the preliminary search report|Effective date: 20171208 |
    2018-06-28| PLFP| Fee payment|Year of fee payment: 3 |
    2020-06-29| PLFP| Fee payment|Year of fee payment: 5 |
    2021-06-29| PLFP| Fee payment|Year of fee payment: 6 |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1655059A|FR3052171B1|2016-06-03|2016-06-03|PROCESS FOR EXTRACTING RARE EARTHS CONTAINED IN PERMANENT MAGNETS|FR1655059A| FR3052171B1|2016-06-03|2016-06-03|PROCESS FOR EXTRACTING RARE EARTHS CONTAINED IN PERMANENT MAGNETS|
    PCT/FR2017/051399| WO2017207947A1|2016-06-03|2017-06-02|Method for extracting rare earth elements contained in permanent magnets|
    US16/306,612| US11155898B2|2016-06-03|2017-06-02|Method for extracting rare earth elements contained in permanent magnets|
    EP17735187.1A| EP3464655A1|2016-06-03|2017-06-02|Method for extracting rare earth elements contained in permanent magnets|
    CA3022190A| CA3022190A1|2016-06-03|2017-06-02|Method for extracting rare earth elements contained in permanent magnets|
    US17/397,612| US20210363608A1|2016-06-03|2021-08-09|Method For Extracting Rare Earth Elements Contained In Permanent Magnets|
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